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公开(公告)号：US5783052A
公开(公告)日：1998-07-21
申请号：US820260
申请日：1997-03-18
CPC分类号： C25B9/08 , C02F1/46109 , C02F1/4618 , C02F1/4674 , C02F2001/46138 , C02F2001/46152 , C02F2201/003 , C02F2201/46115 , C02F2209/04 , C02F2209/06 , C02F2303/04
摘要： An electrochemical cell for the treatment of water and/or water solutions comprises an internal electrode having a middle section and a pin-end at each end thereof, the diameter of each pin-end being not more than 0.75 of the diameter of the middle section; an external electrode mounted around the internal electrode; and a coaxial ceramic diaphragm mounted in a separate inter-electrode space in an electrode chamber of the cell. The external electrode is mounted in lower and upper dielectric bushings. Both the internal electrode and the external electrode are connected with positive and negative poles of a power supply. The cell further includes an upper dielectric collector head and a lower dielectric collector head which each have an axial channel; each collector head being installed in the bushing slots and adapted for turning therein. The diaphragm being fastened by elastic gaskets mounted in the slots of the bushings. The diameter of the middle section of the internal electrode being defined by the formula: 2M
摘要翻译： 用于处理水和/或水溶液的电化学电池包括内部电极，每个端部具有中间部分和销端，每个销端的直径不大于中间部分直径的0.75 ; 安装在内部电极周围的外部电极; 以及安装在电池的电极室中的分离的电极间空间中的同轴陶瓷膜。 外部电极安装在下部和上部电介质衬套中。 内部电极和外部电极均与电源的正极和负极连接。 电池还包括每个具有轴向通道的上介电收集器头和下介电收集器头; 每个收集头安装在衬套槽中并适于在其中转动。 隔膜通过安装在衬套的槽中的弹性垫圈紧固。 内部电极的中间部分的直径由下式定义：2M
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2.发明授权Apparatus for obtaining products by anode oxidation of dissolved chlorides of alkaline or alkaline-earth metals 失效用于通过碱性或碱土金属的溶解氯阳极氧化获得产物的装置
公开(公告)号：US06004439A
公开(公告)日：1999-12-21
申请号：US44951
申请日：1998-03-19
CPC分类号： C25B9/06
摘要： An electrochemical cell or a plurality or block of electrochemical cells is connected through an anode circulation system to a reservoir which is also provided with a built-in controller for maintaining the level of anolyte. The built-in controller can be any suitable regulation device that controls the speed at which the brine is pumped into the anode chamber. A valve-type device is provided on the reservoir for releasing the gaseous mixture of the oxidants to maintain a given pressure in the anode circulation system. The cathode circulation system also includes a reservoir which also includes a valve-type device for the discharge of the excess gas-liquid mixture. A feed unit which contains a pump and a brine tank is connected to the lower part of the anode circulation system. A gas separator for separating hydrogen from the alkaline solution (the catholyte) is also connected to the system.
摘要翻译： 电化学电池或多个或多个电化学电池通过阳极循环系统连接到还具有用于维持阳极电解液水平的内置控制器的储存器。 内置控制器可以是控制盐水泵入阳极室的速度的任何合适的调节装置。 在储存器上设置阀式装置，用于释放氧化剂的气体混合物，以在阳极循环系统中保持给定的压力。 阴极循环系统还包括储存器，其还包括用于排出过量气体 - 液体混合物的阀式装置。 包含泵和盐水箱的进料单元连接到阳极循环系统的下部。 用于从碱性溶液（阴极电解液）分离氢的气体分离器也连接到系统。
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公开(公告)号：US5635040A
公开(公告)日：1997-06-03
申请号：US613968
申请日：1996-03-11
CPC分类号： C25B9/08 , C02F1/46109 , C02F1/4618 , C02F1/4674 , C02F2001/46138 , C02F2001/46152 , C02F2201/003 , C02F2201/46115 , C02F2209/04 , C02F2209/06 , C02F2303/04
摘要： An electrochemical cell for the treatment of water and/or water solutions comprises an internal electrode having a middle section and a pin-end at each end thereof, the diameter of each pin-end being not more than 0.75 of the diameter of the middle section; an external electrode mounted around the internal electrode; and a coaxial ceramic diaphragm mounted in a separate inter-electrode space in an electrode chamber of the cell. The external electrode is mounted in lower and upper dielectric bushings. Both the internal electrode and the external electrode are connected with positive and negative poles of a power supply. The cell further includes an upper dielectric collector head and a lower dielectric collector head which each have an axial channel; each collector head being installed in the bushing slots and adapted for turning therein. The diaphragm being fastened by elastic gaskets mounted in the slots of the bushings. The diameter of the middle section of the internal electrode being defined by the formula:2M
摘要翻译： 用于处理水和/或水溶液的电化学电池包括内部电极，每个端部具有中间部分和销端，每个销端的直径不大于中间部分直径的0.75 ; 安装在内部电极周围的外部电极; 以及安装在电池的电极室中的分离的电极间空间中的同轴陶瓷膜。 外部电极安装在下部和上部电介质衬套中。 内部电极和外部电极均与电源的正极和负极连接。 电池还包括每个具有轴向通道的上介电收集器头和下介电收集器头; 每个收集头安装在衬套槽中并适于在其中转动。 隔膜通过安装在衬套的槽中的弹性垫圈紧固。 内部电极的中间部分的直径由下式定义：2M
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公开(公告)号：US5540819A
公开(公告)日：1996-07-30
申请号：US435524
申请日：1995-05-05
申请人： Vitold M. Bakhir , Viktor G. Vedenkov , Boris I. Leonov , Vladimir I. Prilutsky , Evgeny A. Repetin , Jury G. Zadorozhny , Nikolai N. Naida , Oleg A. Mashkov , Nugzar V. Dzheiranishvili , Sergei K. Butin
发明人： Vitold M. Bakhir , Viktor G. Vedenkov , Boris I. Leonov , Vladimir I. Prilutsky , Evgeny A. Repetin , Jury G. Zadorozhny , Nikolai N. Naida , Oleg A. Mashkov , Nugzar V. Dzheiranishvili , Sergei K. Butin
IPC分类号： C02F1/46 , C02F1/28 , C02F1/461 , C02F1/467 , C02F9/00 , C02F101/20 , C02F101/30
CPC分类号： C02F1/46104 , C02F1/283 , C02F1/4674 , C02F2101/20 , C02F2201/4611 , C02F2201/46115 , C02F2201/4617 , C02F2303/04 , C02F9/00
摘要： There is proposed a water treatment method by causing the water to be pured to flow through a first and a second compartments arranged in succession in an electrolysis cell divided by a permeable membrane into said first and second compartments. Each of the compartments accomodates an electrode, one of them being an anode, and the other--a cathode. Direct electric current is then passed through the water between the anode and the cathode, the current value being determined from the following equation:I=K.times.(C).sup.1/4 .times.Q,whereinI is the current amperage (A),C is the feed water mineralization equal to 0.1-1.5 g/l,Q is the water flow rate (1/hour), ##EQU1## the I/Q ratio being comprised within from about 110 to about 220 Coulomb/liter. The water is caused to flow successively from the anode compartment towards the cathode compartment. Once the water is discharged from the cathode compartment, it is subjected to filtering by passing the water through a bed of a porous carbonaceous material.
摘要翻译： 提出了一种水处理方法，该方法是通过使被净化的水流过第一和第二隔室，所述第一和第二隔室依次排列在由渗透膜分隔的电解槽中而连接到所述第一和第二隔室中。 每个隔室都容纳一个电极，其中一个是阳极，另一个是阴极。 然后直接电流通过阳极和阴极之间的水，电流值由下式确定：I = Kx（C）+ E，fra 1/4 + EE xQ，其中I是电流安培数 A），C是给水矿化度等于0.1-1.5g / l，Q是水流量（1 /小时），I / Q比值在约110至约220库仑/升 。 导致水从阳极室朝向阴极室依次流动。 一旦水从阴极室排出，通过使水通过多孔碳质材料床进行过滤。
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公开(公告)号：US4334987A
公开(公告)日：1982-06-15
申请号：US212087
申请日：1980-11-27
申请人： Ulmas D. Mamadzhanov , Vitold M. Bakhir , Vladimir I. Klimenko , Jury G. Zadorozhny , Stanislav A. Alekhin
发明人： Ulmas D. Mamadzhanov , Vitold M. Bakhir , Vladimir I. Klimenko , Jury G. Zadorozhny , Stanislav A. Alekhin
CPC分类号： B03B5/00 , B01D43/00 , B01D57/02 , B03C5/02 , E21B21/065
摘要： The method of separating the solid phase in a drilling mud includes forming from the drilling mud an adhesion layer 2 on a rotated curvilinear closed surface 3 partly projected into the drilling mud. Then a portion of this adhesion layer is separated onto another rotated curvilinear closed surface 5 positioned to contact a portion of the adhesion layer 2. The respective linear speeds of the adhesion layer 2 and of said another rotating closed curvilinear surface 5 in the area of their contact are selected to be substantially equal. The method of the invention provides for regulating the separation of the solid phase in drilling mud within a wide range depending on the mineralogical composition thereof.
摘要翻译： PCT No.PCT / SU79 / 00128 Sec。 371日期：1980年11月27日 102（e）日期1980年9月17日PCT申请日1979年11月27日PCT公布。 第WO80 / 02041号公报 日期为1980年10月2日。在钻井泥浆中分离固相的方法包括从钻井泥浆中将部分投影到钻井泥浆中的旋转的曲线闭合表面3上的粘附层2形成。 然后，该粘合层的一部分被分离到另一旋转的曲线闭合表面5上，定位成接触粘附层2的一部分。粘合层2和所述另一个旋转的闭合曲线表面5在它们的区域中的相应线速度 接触被选择为基本相等。 本发明的方法提供了根据其矿物学成分在很宽的范围内调节钻井泥浆中固相的分离。
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公开(公告)号：US5985110A
公开(公告)日：1999-11-16
申请号：US76656
申请日：1998-05-12
CPC分类号： C02F1/4618 , C02F1/001 , C02F2001/46138 , C02F2001/46152 , C02F2201/003 , C02F2201/4611 , C02F2201/46115 , C02F2201/4618 , C02F2209/04 , C02F2209/06 , C02F2303/04
摘要： An apparatus for electrochemical purification of water and for regulation of acid-alkaline properties, Red-Ox characteristics and catalytic activity of water that can be used for obtaining washing and disinfecting solutions. The apparatus includes at least one electrochemical cell which contain vertical coaxial cylindrical and rod electrodes made from material nonsoluble during electrolysis and an ultrafiltration ceramic diaphragm installed between the electrodes to create inter-electrode space in the electrode chambers. Channels for the treated solution supply into and discharge from the electrode chambers. A feeding line is connected to the inlet of the negative electrode chamber and the output of the negative electrode chamber is connected to the inlet of the positive electrode chamber by a special line which has a by-pass for discharging a part of the degasified treated solution from the chamber of the negative electrode. A catalyst chamber can be installed on the special line. The catalyst chamber contains a mixture of particles of carbon and manganese dioxide. A separator with a tangential inlet is used for discharging a part of the degasified processed solution.
摘要翻译： 用于电化学纯化水的装置，用于调节酸碱性质，Red-Ox特性和可用于获得洗涤和消毒溶液的水的催化活性。 该装置包括至少一个电化学电池，其包含由电解期间不可溶的材料制成的垂直同轴圆柱形和棒状电极，以及安装在电极之间的超滤陶瓷膜，以在电极室中产生电极间空间。 经处理溶液的通道供应入电极室并从电极室排出。 馈电线连接到负极室的入口，负极室的输出端通过专门的线路连接到正极室的入口，该专线具有用于排出部分脱气处理溶液的旁路 从负极室。 催化剂室可以安装在专线上。 催化剂室含有碳和二氧化锰颗粒的混合物。 具有切向入口的分离器用于排出部分脱气处理溶液。
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公开(公告)号：US5871623A
公开(公告)日：1999-02-16
申请号：US820259
申请日：1997-03-18
CPC分类号： C02F1/4618 , C02F1/001 , C02F1/4674 , C02F2001/46138 , C02F2001/46152 , C02F2201/003 , C02F2201/4611 , C02F2201/46115 , C02F2201/4618 , C02F2209/04 , C02F2209/06 , C02F2303/04
摘要： An apparatus for electrochemical purification of water and for regulation of acid-alkaline properties, Red-Ox characteristics and catalytic activity of water that can be used for obtaining washing and disinfecting solutions. The apparatus includes at least one electrochemical cell which contain vertical coaxial cylindrical and rod electrodes made from material nonsoluble during electrolysis and an ultrafiltration ceramic diaphragm installed in the bushings between the electrodes to create inter-electrode space in the electrode chambers. The lower and upper bushings have a channels for the treated solution supply into and discharge from the electrode chambers. The channels are connected to the feeding and discharging adjustment lines. There is also a metering pump on the water line for sodium chloride dosing into the water to be treated. The water line contains a flow regulator connected to the feeding and discharging adjustment lines. Poles of the power supply are connected to the electrodes. The feeding line is connected to the inlet of the negative electrode chamber and the output of the negative electrode chamber is connected to the inlet of the positive electrode chamber by a special line which has an adjustment for discharging a part of the degasified treated solution from the chamber of the negative electrode. A catalyst chamber can be installed on the special line. The catalyst chamber contains a mixture of particles of carbon and manganese dioxide. A separator with a tangential inlet is used for discharging a part of the degasified processed solution.
摘要翻译： 用于电化学纯化水的装置，用于调节酸碱性质，Red-Ox特性和可用于获得洗涤和消毒溶液的水的催化活性。 该装置包括至少一个电化学电池，其包含由在电解过程中不相容的材料制成的垂直同轴圆柱形和棒状电极以及安装在电极之间的衬套中的超滤陶瓷膜，以在电极室中产生电极间空间。 下部和上部衬套具有用于经处理的溶液供给电极室和从电极室排出的通道。 通道连接到进给和排料调节线。 在水线上还有一个计量泵，用于将氯化钠投入到待处理的水中。 水管线包括连接到进料和排料调节管线的流量调节器。 电源极与电极连接。 馈电线连接到负极室的入口，负极室的输出端通过专用线连接到正极室的入口，该专线具有用于从一部分脱气处理溶液中排出一部分 负极室。 催化剂室可以安装在专线上。 催化剂室含有碳和二氧化锰颗粒的混合物。 具有切向入口的分离器用于排出部分脱气处理溶液。
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公开(公告)号：US5427667A
公开(公告)日：1995-06-27
申请号：US157039
申请日：1994-03-25
申请人： Vitold M. Bakhir , Jury G. Zadorozhny , Jury A. Rakhmanin , Igor N. Naida , Nikolai N. Naida , Nugzar V. Dzheiranishvili , Boris I. Leonov , Sergei K. Butin , Viktor G. Vedenkov
发明人： Vitold M. Bakhir , Jury G. Zadorozhny , Jury A. Rakhmanin , Igor N. Naida , Nikolai N. Naida , Nugzar V. Dzheiranishvili , Boris I. Leonov , Sergei K. Butin , Viktor G. Vedenkov
IPC分类号： C02F1/46 , C02F1/00 , C02F1/461 , C02F1/467 , C02F1/76 , C25B1/10 , C25B1/26 , C25B9/00 , C25B9/06 , C25B9/08 , C25B11/02
CPC分类号： C02F1/4618 , C02F1/46104 , C02F1/001 , C02F1/4674 , C02F2001/46138 , C02F2001/46152 , C02F2201/003 , C02F2201/4611 , C02F2201/46115 , C02F2201/46145 , C02F2303/04 , C02F2303/185 , Y02E60/366
摘要： An apparatus for electrical treatment of water can be used for purifying and disinfecting potable water, and also for producing detergent and disinfecting solutions, and comprises at least one electrochemical cell made up of an upright cylindrical electrode and a rod electrode of a variable cross-section mounted coaxially in dielectric sleeves, an ultrafiltration diaphragm made from ceramics based on zirconium oxide and coaxially mounted in the sleeves between the electrodes, the geometrical dimensions of the cell meet some definite relationships. The system of openings in the electrodes and ducts in the sleeves provides for the optimal hydraulic characteristics of the cell. The sleeves and cylindrical electrode have the same external diameter and the cells are specially secured by means of gaskets in the upper and lower headers of a dielectric material with cylindrical sockets in each and supply and discharge ducts. The headers have several sockets each or are made as a built-up structure composed of units having one socket each, and are provided with means for sealing and bracing the structure, and the cells accommodated in the sockets are hydraulically connected in parallel and electrically connected in parallel and series-parallel. The apparatus can also comprise flow rate control devices adapted to meter a reagent and mounted at the water supply line, containers with a catalyst and a hydraulic connection. The apparatus permits of reducing the electric power consumption, simplifying the design, reducing labour expenditures in assembly and disassembly of the apparatus, and also makes it possible to widen the functional potentialities due to simplifying and unifying the hydraulic system of the apparatus.
摘要翻译： PCT No.PCT / RU93 / 00075 Sec。 371日期：1994年3月25日 102（e）1994年3月25日PCT 1993年3月26日PCT公布。 公开号WO93 / 20014 PCT 日期为1993年10月14日。电水处理装置可用于净化消毒饮用水，还可用于生产洗涤剂和消毒溶液，并且包括至少一个电化学电池，其由直立的圆柱形电极和棒 电介质套筒同轴安装的可变截面电极，由基于氧化锆的陶瓷制成的超滤膜片，并同轴地安装在电极之间的套筒中，电池的几何尺寸符合一定的关系。 套管中的电极和管道中的开口系统提供电池的最佳水力特性。 袖子和圆柱形电极具有相同的外径，并且电池通过垫圈特别地固定在介电材料的上和下集管中，每个电介质材料和每个供应和排放管道中都有圆柱形插座。 集管具有多个插座，或者由构成的结构构成，该结构由具有一个插座的单元组成，并且设置有用于密封和支撑结构的装置，并且容纳在插座中的电池被液压连接并电连接 并联和串联。 该装置还可以包括流量控制装置，其适于计量试剂并安装在供水管线处，具有催化剂和液压连接的容器。 该装置允许减少电力消耗，简化设计，减少装置的组装和拆卸中的人力开支，并且还可以由于简化和统一装置的液压系统而扩大功能潜力。
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公开(公告)号：US4400266A
公开(公告)日：1983-08-23
申请号：US224548
申请日：1980-11-27
申请人： Ulmas D. Mamadzhanov , Vitold M. Bakhir , Vladimir I. Klimenko , Stanislav A. Alekhin , Jury G. Zadorozhny
发明人： Ulmas D. Mamadzhanov , Vitold M. Bakhir , Vladimir I. Klimenko , Stanislav A. Alekhin , Jury G. Zadorozhny
CPC分类号： B03C5/02 , B01D43/00 , E21B21/065
摘要： A method for separating solid phase from drilling mud, comprising forming from drilling mud and adhesive layer on a rotary closed curvilinear surface partly placed in the drilling mud, with subsequent feeding of an ionized gas jet along a tangent line to the adhesive layer, the gas jet entraining and removing solid phase particles from the drilling mud. The linear velocity of the adhesive layer in the zone of its contact with the gas jet is controlled by changing the velocity of the gas jet. An apparatus for carrying out the method comprises: a tank filled with drilling mud and accommodating a drum installed for rotation for forming an adhesive layer of drilling mud on its cylindrical surface during rotation of the drum; a nozzle which is arranged in parallel to a tangent line to the drum surface and communicates with a source of a gas under pressure for forming a jet of gas that entrains and removes solid phase particles from the drilling mud; a pair of electrodes connected to a high-voltage d-c supply source for ionizing the gas jet.
摘要翻译： PCT No.PCT / SU80 / 00054 Sec。 371日期：1980年11月27日 102（e）1980年11月25日PCT PCT Fils 3月26日PCT公布。 出版物WO80 / 02047 日期：1980年10月2日。一种用于从钻井泥浆中分离固相的方法，包括从部分放置在钻井泥浆中的旋转闭合曲线表面上的钻井泥浆和粘合剂层形成，随后沿着切线进行电离气体射流 到粘合剂层，气体夹带和从钻井泥浆中除去固相颗粒。 通过改变气体射流的速度来控制与气体射流接触的区域中的粘合剂层的线速度。 一种用于执行该方法的装置，包括：在滚筒旋转期间，填充钻井泥浆并容纳安装用于旋转的罐的罐，用于在其圆柱形表面上形成钻井泥浆的粘合剂层; 喷嘴，其平行于与滚筒表面的切线平行设置，并与加压气体源连通，以形成夹带并从钻井泥浆中除去固相颗粒的气体射流; 连接到用于电离气体射流的高电压d-c电源的一对电极。
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公开(公告)号：US4323445A
公开(公告)日：1982-04-06
申请号：US224547
申请日：1980-11-26
申请人： Stanislav A. Alekhin , Eduard B. Kuznetsov , Vitold M. Bakhir , Vladimir I. Klimenko , Jury G. Zadorozhny
发明人： Stanislav A. Alekhin , Eduard B. Kuznetsov , Vitold M. Bakhir , Vladimir I. Klimenko , Jury G. Zadorozhny
CPC分类号： C02F1/4696 , B01D57/02 , B30B9/12 , C02F11/006 , E21B21/065 , C02F2103/10 , Y10S209/913
摘要： An apparatus for electrokinetically separating drilling mud into liquid and solid phases comprising a casing (1) having an inlet (2) for drolling mud and outlets (3,13) for separated phases thereof and accommodating electrodes connected to the negative terminal and to the positive terminal, respectively, of a d-c source (8). The electrode connected to the negative terminal of the d-c source (8) comprises a conveyor screw (4) which has a cylindrical portion (5) and an adjacent conical portion (6). The casing (1) functions as the electrode connected to the positive terminal of the d-c source (8) and has respective cylindrical (10a, 10b, 10c) and conical (11) portions. The outlet (13) for solid phase of drilling mud is provided at the end of the conical portion (11) of the casing (1). There is provided a receptacle (14) for collecting solid phase of drilling mud communicating with the outlet (13) for solid phase of drilling mud provided in the casing (1).
摘要翻译： 一种用于将钻井泥浆电动分离成液体和固相的装置，包括具有用于排出泥浆和出口（3,13）的入口（3）的壳体（1），用于分离相，并且容纳连接到负极端子的阳极和阳极 端子，分别为直流源（8）。 连接到d-c源（8）的负端子的电极包括具有圆柱形部分（5）和相邻圆锥形部分（6）的输送螺杆（4）。 壳体（1）用作连接到d-c源（8）的正极端子的电极，并且具有相应的圆柱形（10a，10b，10c）和圆锥形部分（11）。 用于钻井泥浆固相的出口（13）设置在壳体（1）的锥形部分（11）的端部。 设置有用于收集与出口（13）连通的钻井泥浆的固相以用于设置在壳体（1）中的钻井泥浆的固相的容器（14）。
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